CN207227067U - A kind of new oily-water seperating equipment - Google Patents
A kind of new oily-water seperating equipment Download PDFInfo
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- CN207227067U CN207227067U CN201720751208.6U CN201720751208U CN207227067U CN 207227067 U CN207227067 U CN 207227067U CN 201720751208 U CN201720751208 U CN 201720751208U CN 207227067 U CN207227067 U CN 207227067U
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Abstract
The utility model discloses a kind of new oily-water seperating equipment, including babinet, the babinet top is equipped with inlet tube and oil exit pipe, and lower part is equipped with discharge outlet, and middle part is equipped with the secondary drainage mouth that can be periodically turned on；The flow-stopping plate tilted upward is equipped with the babinet below inlet tube, the secondary drainage mouth is located at the secondary separation room lower part being made of babinet and secondary oil dividing plate, and the secondary oil dividing plate is equipped with overflow pipe；M types coalescing-plate group adjustable in pitch is equipped with the babinet, cabinet wall is fixed on by fixed plate at the top of the M types coalescing-plate group, side is fixed by side shield, the bottom of box is fixed in bottom by foundation, device coalescence plate spacing disclosed in the utility model adjusts, and is suitable for the separation of the grease of different viscosities, disposal ability is big, oil removal efficiency is high, has good application prospect.
Description
Technical field
Oily water separating equipment field is the utility model is related to, more particularly to a kind of new oily-water seperating equipment.
Background technology
Oily wastewater of the Produced Liquid in oil field after three phase separator separates by settling tank, it is necessary to further settle
Separation, at present mainly there is oils existing forms in oily wastewater：(1) floating oil：Particle diameter >=100 micron, slightly take standing or half
The method of standing, you can float on the water surface and be easy to remove；(2) dispersed oil：Particle diameter is at 10 100 microns, if enough quiet
Put the time, oil droplet can also shift to the water surface, need to generally stand 12 it is small when more than, oily removal rate is more than 80%；(3) oil emulsion：
About 0.1 to 10 micron of particle diameter, has certain stability, is merely that can not separate itself and water by gravitational settling, it is necessary to through broken
It could be separated after breast or flocculation, seriously affect production.
If separating treatment is carried out, it is necessary to add flocculant, flocculation aid to the oil emulsion in oily wastewater by traditional method
And reverse demulsifier.If the sewage quantity containing oil emulsion of required processing is very big, then certainly will will consume substantial amounts of manpower, financial resources
And material resources.Oily waste water treatment technology improves at present, and biochemical treatment oily wastewater technology has been obtained for very well
Ground application, but the oil emulsion problem in settling tank does not solve also, and the biochemical treatment to sewage plant brings burden.
Utility model content
In order to solve the above technical problems, the utility model provides a kind of new oily-water seperating equipment, to reach separation effect
Fruit is good, and separative efficiency is high, and the residence time is short, the big purpose of disposal ability.
To reach above-mentioned purpose, the technical solution of the utility model is as follows：
A kind of new oily-water seperating equipment, including babinet, the babinet top are equipped with inlet tube and oil exit pipe, and lower part is equipped with
Discharge outlet, middle part are equipped with the secondary drainage mouth that can be periodically turned on；It is equipped with what is tilted upward on the babinet below inlet tube
Flow-stopping plate, the secondary drainage mouth are located at the secondary separation room lower part being made of babinet and secondary oil dividing plate, the secondary point of oil
Plate is equipped with overflow pipe；M types coalescing-plate group adjustable in pitch is equipped with the babinet, the M types coalescing-plate group top passes through solid
Fixed board is fixed on cabinet wall, and side is fixed by side shield, and the bottom of box is fixed in bottom by foundation.
In such scheme, the M types coalescing-plate group includes the coalescing-plate several stacked on top together, the coalescing-plate bag
The coalescing-plate body that cross section is M types is included, the coalescing-plate body is in wavy, the M types top of the coalescing-plate body along longitudinal direction
Oil slick hole is equipped with wavy wave crest along longitudinal direction on end, trough is equipped with raised stepped fore-set, the coalescing-plate sheet
The M type bottom centers of body distribute sedimentation hole along the longitudinal；The back side of the coalescing-plate body is located at the lower orientation of stepped fore-set
Put place and be equipped with stepped groove, the side of the stepped groove is equipped with groove, and the stepped fore-set front end of lower floor's coalescing-plate can be inserted into upper strata
In the stepped groove or groove of coalescing-plate.
In such scheme, the inlet tube and oil exit pipe are L-type, and the outlet of the inlet tube is positioned at the upper of flow-stopping plate
Side；The oil exit pipe is installed on babinet by the oil discharge outlet of babinet, and the apical position of the mouth of pipe is less than the top of M type coalescing-plate groups
Position.
In such scheme, the secondary oil dividing plate is L-type, and overflow pipe is setting up and down in the bottom of L-type, the mouth of pipe of overflow pipe
Apical position is less than the spout tops position of oil exit pipe.
In such scheme, the flow-stopping plate is welded on babinet, and horizontal by 45° angle.
In such scheme, the contact surface of the fixed plate and coalescing-plate is in M types, and any section of contact surface is in wave
Shape, can be at a fully engaged with coalescing-plate.
In such scheme, the position of the discharge outlet is less than the least significant end position of M type coalescing-plate groups.
Through the above technical solutions, new oily-water seperating equipment provided by the utility model can according to it is separated can according to point
From grease viscosity different adjustment coalescing-plate between spacing, to adapt to the requirement of different viscosities grease, good separating effect, point
From efficient, the residence time is short, and disposal ability is big, and floor space is small, meet water-oil separating to it is efficient, miniaturization become
Gesture.It is in particular in：
(1) Gravity Separation farthest improves oil removal efficiency after coalescence technology is combined.
(2) horizontal stream water intake mode, increases coalescence area, and to force current to be formed special for the tortuous passageway of coalescing-plate
Fluidised form so that increase stream pearl between collision probability, promote it is small trip pearl coalescence.
Brief description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described.
Fig. 1 is a kind of new oily-water seperating equipment dimensional structure diagram disclosed in the utility model embodiment；
Fig. 2 is the new oily-water seperating equipment front view disclosed in the utility model embodiment；
Fig. 3 is coalescence plate structure schematic diagram；
Fig. 4 is the top view of Fig. 3；
Fig. 5 is section plan where the stepped fore-set of the coalescing-plate disclosed in the utility model embodiment；
Fig. 6 is A-A diagrammatic cross-sections in Fig. 3；
Fig. 7 is the schematic cross-section that the stepped fore-set of next strata knot tying is inserted into the stepped groove of last layer coalescing-plate；
Fig. 8 is part B enlarged diagram in Fig. 7；
The schematic cross-section of the groove of the stepped fore-set insertion last layer coalescing-plate of the next strata knot tyings of Fig. 9；
Figure 10 is C portion enlarged diagram in Fig. 9.
In figure, 1, coalescing-plate body；2nd, oil slick hole；3rd, stepped fore-set；4th, sedimentation hole；5th, stepped groove；6th, groove；7th, it is solid
Fixed board；8th, foundation；9th, side shield；10th, M types coalescing-plate group；11st, babinet；12nd, secondary drainage mouth；13rd, overflow pipe；14th, secondary point
Oiled-plate method；15th, oil exit pipe；16th, inlet tube；17th, flow-stopping plate；18th, discharge outlet.
Embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describe.
The utility model provides a kind of new oily-water seperating equipment, and structure as depicted in figs. 1 and 2, which will weight
Force method is combined with coalescence technology, improves hydraulics, enhances the state of the water-oil separating of oil emulsion.
Oily-water seperating equipment as depicted in figs. 1 and 2, including babinet 11,11 top of babinet are equipped with inlet tube 16 and oil extraction
Pipe 15, lower part are equipped with discharge outlet 18, and middle part is equipped with the secondary drainage mouth 12 that can be periodically turned on；It is located on babinet 11 under inlet tube 16
Side is welded with the flow-stopping plate 17 set horizontal by 45° angle, and secondary drainage mouth 12 is located at by babinet 11 and secondary oil dividing plate 14
The secondary separation room lower part of composition, secondary oil dividing plate 14 are L-type, are welded on the upper left of babinet 11, second for grease
Secondary separation；Overflow pipe 13 is setting up and down in the bottom of L-type, and the spout tops position of overflow pipe 13 is less than the mouth of pipe top of oil exit pipe 15
End position.
Inlet tube 16 and oil exit pipe 15 are L-type, and the outlet of inlet tube 16 is positioned at the top of flow-stopping plate 17；Oil exit pipe 15 is logical
The oil discharge outlet for crossing babinet 11 is installed on babinet 11, and the apical position of the mouth of pipe is less than the apical position of M type coalescing-plates group 10.
M types coalescing-plate group 10 adjustable in pitch is equipped with babinet 11, the top of M type coalescing-plates group 10 is fixed by fixed plate 7
In 11 inner wall of babinet, side is fixed by side shield 9, and 11 bottom of babinet is fixed in bottom by foundation 8.Fixed plate 7 and coalescence
The contact surface of plate is in M types, and any section undulate of contact surface, can be at a fully engaged with coalescing-plate.Side shield 9 welds
In on babinet 11, for fixing M type coalescing-plates group 10, prevent the movement of M type coalescing-plates group 10 or so, its can regular length be M
Length+the 5mm of type coalescing-plate group 10.
M type coalescing-plates group 10 includes the coalescing-plate 60 stacked on top together, and coalescence is adjusted according to the difference of spacing
The quantity of plate.As shown in Figures 3 to 10, coalescing-plate includes the coalescing-plate body 1 that cross section is M types, as shown in fig. 6, coalescing-plate
Body 1 is in wavy along longitudinal direction, and oil slick hole 2 is equipped with wavy wave crest along longitudinal direction on the M types top of coalescing-plate body 1,
Trough is equipped with raised stepped fore-set 3, and the M type bottom centers of coalescing-plate body 1 distribute (Fig. 4 institutes of sedimentation hole 4 along the longitudinal
Show)；As shown in figure 5, the lower position that the back side of coalescing-plate body 1 is located at stepped fore-set 3 is equipped with stepped groove 5, stepped groove 5
Side be equipped with groove 6,3 front end of stepped fore-set of lower floor's coalescing-plate can be inserted into the stepped groove 5 or groove 6 of upper strata coalescing-plate
It is interior.
Oil slick hole 2 is uniformly arranged on the wave crest of coalescing-plate body 1, and stepped fore-set 3 is uniformly arranged on coalescing-plate body 1
Trough on, sedimentation hole 4 is uniformly distributed on the M type bottom center lines of coalescing-plate body 1.
A stepped fore-set 3 is equipped with coalescing-plate at spacing intervals, as the supporter between plate, on stepped top
The lower section of column 3 is equipped with stepped groove 5, and the side of stepped groove 5 is additionally provided with groove 6, and 3 front end of stepped fore-set of lower floor's coalescing-plate can insert
Enter in the stepped groove 5 or groove 6 of upper strata coalescing-plate, plate group can be held together.Into during assembling between andante, to coalescence
Plate group is adjusted, to adapt to the requirement of conveying different viscosities grease.When conveying low viscosity grease, next laminate upper surface
Stepped fore-set 3 is corresponded in the stepped groove 5 of insertion last layer plate lower surface, and as shown in Figure 7 and Figure 8, plate spacing is H at this time；When
During transfer of highly viscous grease, after 180 ° of the direction horizontal rotation of next laminate, the stepped fore-set 3 of next laminate upper surface corresponds to
It is inserted into the groove 6 of last layer plate lower surface, as shown in Figure 9 and Figure 10, plate spacing is H+A at this time；Completed with this viscous to difference
Spend the conveying requirement of grease.
The board selection polypropylene of coalescing-plate, adds bone meal, to polypropylene board in polypropylene board manufacturing process
Tow sides are modified processing.Modified mechanism is hydroxyl in the positive and negative grafting of basic unit, makes it have strong oleophilic drainage
Characteristic, so as to realize emulsified oil droplet be demulsified after grease rapid coalescence.
Specific separation process is as follows：
Oil emulsion is inputted in babinet 11 with suitable flow by inlet tube 16；Into babinet 11 oil emulsion to flow down
In dynamic process, flow-stopping plate 17 is encountered, and under the action of flow-stopping plate 17, is flowed along 17 direction of flow-stopping plate to upper left side,
So as to avoid oil emulsion from directly flowing to 11 bottom of babinet.
Oil emulsion lateral flow enters M type coalescing-plates group 10, and the surface of coalescing-plate is waveform, its tortuous passageway provided
Very big coalescence surface, generates the current similar to sine wave, makes during tiny oil droplets bottom horizontal flow sheet in coalescing-plate
Surface collision, coalescence, when droplet diameter is coalesced to certain particle diameter, oil slick hole 2 that oil droplet passes through 10 top of M type coalescing-plates group
Start to float, the relatively low mixed liquor of oil content starts to sink by the sedimentation hole 4 of 10 bottom of M type coalescing-plates group.Oil droplet passes through layer
Strata knot tying gradually floats up to the top of babinet 11, and the relatively low mixed liquor of oil content sinks down into 11 bottom of babinet by coalescing-plate layer by layer
Portion, is discharged from discharge outlet 18, is floated up to the oil droplet at the top of babinet 11 and can be exported by oil exit pipe outside babinet 11, carries out oil droplet
Recycle for the first time.
The relatively low mixed liquor of 11 bottom oil content of babinet is secondary into being formed by secondary oil dividing plate 14 via overflow pipe 13
Separation chamber, under the effect of gravity, mixed liquor form layering, and the of a relatively high mixed liquor of oil content is located at top, and oil content phase
Lower part is located to lower mixed liquor, periodically opens secondary drainage mouth 12, the low water of oil content is discharged, forms the second of grease
Secondary separation.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or new using this practicality
Type.A variety of modifications to these embodiments will be apparent for those skilled in the art, determine herein
The General Principle of justice can be realized in other embodiments without departing from the spirit or scope of the present utility model.Cause
This, the utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein
The most wide scope consistent with features of novelty.
Claims (7)
1. a kind of new oily-water seperating equipment, it is characterised in that including babinet, the babinet top is equipped with inlet tube and oil extraction
Pipe, lower part are equipped with discharge outlet, and middle part is equipped with the secondary drainage mouth that can be periodically turned on；It is equipped with the babinet below inlet tube
The flow-stopping plate tilted upward, the secondary drainage mouth are located at the secondary separation room lower part being made of babinet and secondary oil dividing plate, institute
State secondary oil dividing plate and be equipped with overflow pipe；M types coalescing-plate group adjustable in pitch, the M types coalescing-plate group are equipped with the babinet
Cabinet wall is fixed in top by fixed plate, and side is fixed by side shield, and the bottom of box is fixed in bottom by foundation.
2. a kind of new oily-water seperating equipment according to claim 1, it is characterised in that the M types coalescing-plate group includes
The coalescing-plate of several stacked on top together, the coalescing-plate include the coalescing-plate body that cross section is M types, the coalescing-plate sheet
Body is in wavy along longitudinal direction, and oil slick hole, ripple are equipped with wavy wave crest along longitudinal direction on the M types top of the coalescing-plate body
Paddy is equipped with raised stepped fore-set, and the M type bottom centers of the coalescing-plate body distribute sedimentation hole along the longitudinal；It is described poly-
The lower position that the back side of knot tying body is located at stepped fore-set is equipped with stepped groove, and the side of the stepped groove is equipped with groove,
The stepped fore-set front end of lower floor's coalescing-plate can be inserted into the stepped groove or groove of upper strata coalescing-plate.
3. a kind of new oily-water seperating equipment according to claim 1, it is characterised in that the inlet tube and oil exit pipe are equal
For L-type, the outlet of the inlet tube is positioned at the top of flow-stopping plate；The oil exit pipe is installed on babinet by the oil discharge outlet of babinet
On, the apical position of the mouth of pipe is less than the apical position of M type coalescing-plate groups.
A kind of 4. new oily-water seperating equipment according to claim 3, it is characterised in that the secondary oil dividing plate is L-type,
Overflow pipe is setting up and down in the bottom of L-type, and the spout tops position of overflow pipe is less than the spout tops position of oil exit pipe.
5. a kind of new oily-water seperating equipment according to claim 1, it is characterised in that the flow-stopping plate is welded in babinet
On, and horizontal by 45° angle.
6. a kind of new oily-water seperating equipment according to claim 1, it is characterised in that the fixed plate and coalescing-plate
Contact surface is in M types, and any section undulate of contact surface, can be at a fully engaged with coalescing-plate.
7. a kind of new oily-water seperating equipment according to claim 1, it is characterised in that the position of the discharge outlet is less than
The least significant end position of M type coalescing-plate groups.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720751208.6U CN207227067U (en) | 2017-06-27 | 2017-06-27 | A kind of new oily-water seperating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720751208.6U CN207227067U (en) | 2017-06-27 | 2017-06-27 | A kind of new oily-water seperating equipment |
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| Publication Number | Publication Date |
|---|---|
| CN207227067U true CN207227067U (en) | 2018-04-13 |
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ID=61852035
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720751208.6U Active CN207227067U (en) | 2017-06-27 | 2017-06-27 | A kind of new oily-water seperating equipment |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108658172A (en) * | 2018-05-23 | 2018-10-16 | 王英华 | A kind of vertical oily-water seperating equipment |
| CN111422949A (en) * | 2020-05-27 | 2020-07-17 | 河北澳科中意环保科技有限公司 | Oil-water separation device |
-
2017
- 2017-06-27 CN CN201720751208.6U patent/CN207227067U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108658172A (en) * | 2018-05-23 | 2018-10-16 | 王英华 | A kind of vertical oily-water seperating equipment |
| CN108658172B (en) * | 2018-05-23 | 2021-05-18 | 临沂宝力佳食品有限公司 | Vertical oil-water separation device |
| CN111422949A (en) * | 2020-05-27 | 2020-07-17 | 河北澳科中意环保科技有限公司 | Oil-water separation device |
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Address after: No.28, Zhejiang Road, Shinan District, Qingdao City, Shandong Province Patentee after: Shandong Ocean Instrument Technology Center Co.,Ltd. Address before: No. 28, Zhejiang Road, Southern District, Shandong, Qingdao, Shandong Patentee before: SHANDONG PROVINCE OCEANOGRAPHIC INSTRUMENTATION TECHNOLOGY CENTER |